Aggregation behavior of nanoparticles in fluidized beds

被引:208
作者
Hakim, LF [1 ]
Portman, JL [1 ]
Casper, MD [1 ]
Weimer, AW [1 ]
机构
[1] Univ Colorado, Dept Chem & Biol Engn, Boulder, CO 80309 USA
基金
美国国家科学基金会;
关键词
fluidization; nanoparticles; dynamic aggregation; vibration; interparticle forces; vacuum;
D O I
10.1016/j.powtec.2005.08.019
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The fluidization behavior of fumed silica, zirconia, and iron oxide nanopowders was studied at atmospheric and reduced pressures. Using a high-speed laser imaging system, the characteristics of fluidized aggregates of nanoparticles were studied in real time. The effect of different particle interactions such as London-van der Waals, liquid bridging and electrostatic on different fluidization parameters was studied at atmospheric pressure. The reduction of interparticle forces resulted in a reduced aggregate size and minimum fluidization velocity (U-mf) and an increased bed expansion. Nanoparticles were also fluidized at reduced pressure (similar to 16 Pa) with vibration to study the effect of low pressure on the minimum fluidization velocity. Aggregate properties (size, density) instead of primary nanoparticle properties were found to govern the minimum fluidization velocity and expansion of the fluidized bed. An important consideration is the relative strength of intra-aggregate interparticle forces (forces within the aggregate holding nanoparticles together) to inter-aggregate interparticle forces (forces between aggregates). This relative strength may be inferred from the sphericity of the aggregates during fluidization. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:149 / 160
页数:12
相关论文
共 71 条
[31]   Characteristics of vibro-fluidization for fine powder under reduced pressure [J].
Mawatari, Y ;
Koide, T ;
Ikegami, T ;
Tatemoto, Y ;
Noda, K .
ADVANCED POWDER TECHNOLOGY, 2003, 14 (05) :559-570
[32]   Effect of particle diameter on fluidization under vibration [J].
Mawatari, Y ;
Koide, T ;
Tatemoto, Y ;
Uchida, S ;
Noda, K .
POWDER TECHNOLOGY, 2002, 123 (01) :69-74
[33]   Comparison of three vibrational modes (twist, vertical and horizontal) for fluidization of fine particles [J].
Mawatari, Y ;
Koide, T ;
Tatemoto, Y ;
Takeshita, T ;
Noda, K .
ADVANCED POWDER TECHNOLOGY, 2001, 12 (02) :157-168
[34]   RECENT WORK ON FLUIDIZED-BED PROCESSING OF FINE PARTICLES AS ADVANCED MATERIALS [J].
MOROOKA, S ;
OKUBO, T ;
KUSAKABE, K .
POWDER TECHNOLOGY, 1990, 63 (02) :105-112
[35]   EFFECT OF INTERPARTICLE FORCES ON EXPANSION OF A HOMOGENEOUS GAS-FLUIDIZED BED [J].
MUTSERS, SMP ;
RIETEMA, K .
POWDER TECHNOLOGY, 1977, 18 (02) :239-248
[36]   Aerated vibrofluidization of silica nanoparticles [J].
Nam, CH ;
Pfeffer, R ;
Dave, RN ;
Sundaresan, S .
AICHE JOURNAL, 2004, 50 (08) :1776-1785
[37]  
NAM CH, 2004, Y11 INT C FLUID ENG
[38]   Flow patterns of fine particles in a vibrated fluidized bed under atmospheric or reduced pressure [J].
Noda, K ;
Mawatari, Y ;
Uchida, S .
POWDER TECHNOLOGY, 1998, 99 (01) :11-14
[39]   Electrode formation by electrophoretic deposition of nanopowders [J].
Ogata, N ;
Van Tassel, J ;
Randall, CA .
MATERIALS LETTERS, 2001, 49 (01) :7-14
[40]   FLUIDIZATION OF FINE AND VERY DENSE HARD-METAL POWDERS [J].
PACEK, AW ;
NIENOW, AW .
POWDER TECHNOLOGY, 1990, 60 (02) :145-158